|Publication number||US2635069 A|
|Publication date||Apr 14, 1953|
|Filing date||Nov 25, 1947|
|Priority date||Nov 25, 1947|
|Publication number||US 2635069 A, US 2635069A, US-A-2635069, US2635069 A, US2635069A|
|Inventors||Dwight L Baker|
|Original Assignee||Ben L Sarett|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (1), Referenced by (17), Classifications (12)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Filed NOV. 25, 1947 2 SHEETS-SHEET 1 April 14, 1953 D. l., BAKER 2,635,069
PRODUCTION OF CATALASE FROM MOLD H0 Zmmvr fwazubzf Cei/fag@ H Z0 n? d i J0 J'oIzds GCI J zz es April 14, 1953 D. L. vBAKER 2,635,069
PRODUCTION OF CATALASE FROM MOLD Filed Nov. 25. 1947 ;2 SHEETS- SHEET 2 JUH IN V EN TOR.
,Ba/fer Patented Apr. 14, 1953 UzNlTED STATES PATENT OFFICE PRGDUGTIQN, 0F CATALASE MQLD DwightL. BakenChicago; Ille., assigner to'V Ben L. Sarett,YChicago,-Ill.
ApplicatiomNovemherrZ, 19,411,fSerialr No. 7884136 teams.. (o1. 19a- 66x ,The present inventiongrelates to. the;- artoi making,,catalaser and tothe provision of' new species of catalase; more specifically.,v it.relates totheproduction of catalase from mold,` and the new forms of catalase obtained thereby.-
It has long been known that catalase occurs.
in most, but not. in all, livingthin-gs. Itsconcentration` varies. enormously, not only from one, form of litel toanother, but even from organgtoI organinthe same livingcreature. In many ,ti ssues,, it occursyonly in traces.
contaminated. withv other enzymes. and biological substances inimical toitsv storage and use under; commercial conditions., VFor` these reasonayit has hithertofore, been impossibile.- to prepare more than trivial quantities oi catalase preriarations.A
Thesefgenerally havexeome from. mammalian aniy purity-, stability. activity and. dependability as.
to. possess real industrial util-ity;
.1. have now discovered that molds.` and; Darf ticularly the species of molds used in the corn.-v mercial-productionof. penicillin, contain; species of,v catalase of great; industrial utility and l; have i invented processes, whereby` said; catalase ube obtained= therefrom in large corrin-iereial'y quanf. Y
titles, and; in preparations of extraordinary potencie, stability; and; industrialutility.
Ihaver found that. the molds. employed the ceinmercial production of penicillin, namely; Pen-z'gzzl'lzumr chrysoeenum and Penicillium no,-
ratzgm, vare excellent seul-.cesr of; new. species;V
of. catala-Se; and thaty Aspergillus niger isf. also; Suelo; a Source.
1; have foundnfurther.; thatv catalase. may be manufacture@ trom, the` spent :moldy remaining as; the hitherto substantially worthless: refuse, i he production; ofi penciljlim which` refuse The invention.l
is available. large; quantities; eleonora-templates the productionof catalasefromA the spent meld resulting from` the; manufacture of. eitrieacid, and' of. gluconic4 acid; as Well as frontr fresh` molds; Specically cultured` for' the manufacture; of catalase.
limits, broader aspectv my invention involve liberating catalase from mold mycelia,. prefer,
ably by; .autolysis;` separating.y the solid cell' resi-V duesfrom. the catalase-bearing. liquor thus ob.
tained; and' purifying said crude catalase.
f-'llleyizorms of; catalase thus obtained, from mold d Where: it does.` occur, it is always entrapped within the cell and.
" areof utility wherever it isl desirable to decornf.
ere new compositions of. metten harina propierties. capabilities' and advantages. distinct. from those ofthe. previously known; eateleses derived from other` sources..v The, eatolases. are enzymes which. catalyze theY decomposition of hydrogen peroxide. into water and.; oxygen, .My new Species of catalase .are operative'throughouta far greater rance of pH eenditiohstheh iSu thefease-with Pre: viously. known Species' ofi catalase.; and. for this reason and others my new species ofv catalase pose. hydrogen peroxide under. industriel condi.- tiohs; eohtrol the time, manner or rete of. de-
composition thereofmr insure quantitatively eomplete removal thereof-` Thos my. new catalase Compositions have o wide. field4 ofginsiustrial utili: ity, and even extend' the use of' hydrogen peroxfide to fields where it hithertofore has not4 been SuitehleV Arnone other applications my' catalase compositions4 are useful inv the arts ofy bleaching,A imparting porosity, andk preventing peroxide formation or rancidity by eliminating`r all traces of hydrogen peroxide Thus' my new centrosi-u tlehs find; enplieationih the menu-facture of loro. feem'rubherfiexliles, feathers, soars. iooda ete.-`
Since my catalase preparations are of namra'l'v vegetable origin and harmless when eaten,A they are specially suitable in foodv technology. For example, they makey it feasible to' useV hydrogen peroxide for raisingbread and cake; for bleaching fruit, `and even oils and fats in which hydrogenperoxide must be completely-removedto prevent subsequent development of rancidity; and
fory preservingv food intermediates in: circulan-Q stances Where it is desired to have the'nal' uct strictly free of preservative. y
As stated above, the invention may advantageously-be realized by operating uponspentmofld Prodobtained as refuse from they commercial produef i tionfofl penicillin.k According toa preferred Inode of' operation, thelivingn mold is filtered, washed, and' treated with a germicide (either organica sueas-toluene, xylenwe,A ethyl acetate, chloroform, etc.,` or-V inorganic, suchas copper' sulphate) tof kill it, hasteneutolllsie, and. Prevent bacterial dei composition. The dead moldy is allowed to autolyze, and the catalase leached from the ruptured cells thereof. If the pH of the autolyzate falls below 6.0i, it is made slightly alkaline to precipitate. acidesolurble. impurities; A
containing. catalase, and an insoluble residue Whichlisdiscarded. Thereafter, the-extract preferably is rnadel mildly` acidto precipitate acid msoluble impurities, which are removed.- A prctein-fractionating` agent is then dissolved the puriedv extract in such. concentrationand under such pH conditionsA that substantially all the catalase; in the extract is precipitated without precipitating much inactive material. Acetone;
ethanol', methanol andammoni-um sulphate are*1 They autoly rzate 1s then separated into a cellfree extractvr suitable fractionating agents. The crude catalase precipitate is collected, and the spent mixture of extract and fractionating agent is discarded. The crude catalase is then re-dissolved in a moderate quantity of aqueous solvent; the solution is made mildly acid; and the catalase is re-precipitated. The catalase thus purified is collected, and is dissolved in a small volume of aqueous solvent, such as water or a mixture of Water and glycerine. Any insoluble matter is removed, leaving a catalase solution of great potency and stability. When necessary, this solution may be preserved against bacterial decomposition by adding conventional germicides. If desired, the puriiied catalase may be obtained in stable solid form by drying the concentrated catalase solution in a vacuum, preferably while maintaining said solution in the frozen state.
lAn important feature of my invention is the step of removing the acid-insoluble impurities, since this usually results, surprisingly enough, in a substantial increase in the total catalase activity of the liquor thus purified.
An even more important feature of the inven- Y tion is the step of precipitating crude catalase from the mother liquor in the absence of acidsoluble impurities, for thereby the yield of total catalase activity may be increased enormously.
Accordingly, one of the principal objects of the present invention is to provide methods for obtaining commercially valuable preparations of catalase.
Another principal object is to provide, in commercially important quantities, new species of catalase having distinctive and valuable properties.
Another object is to provide processes by which the aims of the present invention may be realized through the use of accepted chemical engineering unit processes conducted solely in standard commercial equipment.
Other objects and advantages of the inventionv will be apparent upon further perusal of this specification and the appended claims and drawings.
vIn the drawings:
Figure 1 is a flow sheet illustrating the process set forth in Example I, the principal steps being correspondingly numbered in the iiow sheet and in the example, with optional operations shown in the flow sheet in broken lines; and
Figure 2 isV a chart showing the activity-pH relationship which characterizes penicillium catalase (curve A) and beef liver catalase (curve B).
vAs used herein, the term activity means catalytic activity in decomposing hydrogen peroxide. It is expressed in activity units, one unit of catalase activity decomposing H2O2 under standard arbitrary conditions at a rate such that the activity constant lc isunity in the differential equation Tfks wherein S is the concentration of H2O2 at any instant of time t. Y
The term purity asused herein, means the weight ratio of catalase to the total solids in the preparation--the purity being 1.0 when catalase is the only solid in the preparation.`
The invention will be better appreciated by consideration of the following illustrative examples, which are based upon actual experience with specific representative batches of mold, and
in which many details are specified for the assistance ofthose desiring to practicethe invention.y
It is distinctly to be understood, however, that such details are not to be construed as limitations upon the scope of my invention, which is coextensive with the scope of the appended claims.
Example I Living Penicilliam; chrysogenam which was grown as a source of penicillin, is separated by iiltration from the culture broth into which it has excreted said penicillin, and is Washed free of penicillin, thereby yielding a mat which is sensibly dry to the touch, analyzing from 10% to 25% solids content, and resembling paper pulp of similar water content. In microscopic structure, this mat is a reticulum of mycelia. with considerable water retained in the capillary spaces between the mycelia.
1. AatoZysis.-1,000 pounds of this material, of high solids content, assaying 300,000 units total activity content, pH about '7, is diluted with water to a solids content of 15%, and mixed with about twenty pounds of toluene, the mixing op- Y eration being continued for about three Yhours at room temperature. The mixture is allowed to stand at room temperature for about forty hours more.
In most cases, the pI-I of the slurry is between 6.5 and 7.2 at the end of the autolyzing operation. Sometimes it is much lower. Beginning at pH 5.5, large quantities of inactive protein go into solution. Accordingly, if the pH of the autolyzate is below 6.0, it is raised to between 7.0 and 7.5, for example by the slow addition of concentrated NHiOI-I under constant stirring. This precipitates the acid-soluble matter.
2. Separation of the crude catalase Zqaor. Mixing is resumed; the slurry is diluted to about 10% solids content; from 20 to 50 pounds of infusorial earth or other lter aid is added; and the batch is filtered. The filter cake, which comprises insoluble cell residues and Vprecipitated acid-soluble matter, is washed with water until Isubstantially free of catalase, and is then discarded. The filtrate and washings total about gallons containing 300,000 units of activity, and comprise the cell-free extract or mother liquor.
3. Removal of acid-insoluble impurities- The mother liquor is brought to pH 4.5, for example by very slowly adding glacial acetic acid under constant stirring, about 11/2 gallons ordinarily ybeing required. The liquor is then allowed to stand at room temperature for aboutan hour. In most cases, the solution becomes turbid during acidiiication, and a iocculent precipitate forms in about half an hour. The precipitate is removed, for example by filtration, and discarded. Where acid-insoluble impurities are present, as evinced by the formation of a precipitate, the removal of said acid-insoluble impurities results in an increase in the total activity content of the liquor, the increase in some cases amounting to 100%. In the representative batch illustrated in the flow sheet (Figure l), this step increased the total activity of the liquor from 300,000 units to 350,000 units.
4. First fractionation of catalase- The puriiied mother liquor, amounting to about 100 gallons and having a pH of 4.5, is next mixed at room temperature with about 100 gallons of acetone, thereby precipitating catalase contaminated with some inactive material. The foregoing conditions iachieve a fractional precipitation wherein most of the solids (including much inactive protein) remain in solution, and practically all the catalase is precipitated. This fractionation usually increases the purity of the catalase6 or 7 fold, and surprisingly enoughV it enormously increases the yield o f catalase activity. The total catalase activity in the, Aprecipitate varies from 100% to 1000% of the total catalase activity in thev original extract. In the batch illustrated in Figure 1, the precipitate assayed 1,400,000 units, and weighed about 43 pounds, consisting of about 9 pounds of crude catalase, pounds of lter aid'added to facilitate collection thereof, and 28% pounds of retained liquor and acetone.
This preci-pitate is collected, and dissolved in enough water to make gallons of solution, which usually exhibits a` pH between 4.5 and 5.5-t-he value being 5.2 in the case illustrated in Figure 1. This solution is generally quite unstablewith respect to its catalase activity.
`5". Re-precipitation of catalase-The catalase solution is 'adjusted' to pI-I 4.5, for example by the'gradual addition of glacial acetic acid under constant stirring, and l@ volume of acetone is added-that is, 10 gallons of the aqueous catalase solution are treated with 5 gallons of acetone. A copious precipitate forms, lter aid is added, and the precipitate is collected. This purified precipitate lere-dissolved in approximately four gallons of water. The filter aid is then lteredioii. leaving a( concentrated aqueous solutionl of catalase.y
This second precipitation achieves an enormous purificationof the catalase without diminution in yield. For example, the 9 pounds o1A crude catalase in the precipitate obtained in step 4 of theyb-atchillustrated inFigure l yielded in* lstep 5 a precipitate weighing 51/2 pounds and containingabout 1/2 pound oi' catalase, 11/2 pounds ofvfllter aid,y and 31/2 pounds of retained solvent.
The concentrated solution prepared from the reflned'catalase appeared greenV when viewed by Y light transmitted through it, but brownish when viewedby light reflected from it. It containedy 1,400,000 activity units. In another typical instance, the activity-of the crude catalase was 350 'units per gram, expressed on a dry basis, and the activity of the `refined catalase was 8,000 units per gram, on the same basis.
The concentrated solution may be diluted with Water, glycerine, or the like tov any convenient strength. Solutions of mold catalase in 1:1-,mixtures of water and glycerine are highly resistant to bacterial decomposition, and are well suited for use in food manufacture. Other aqueous preparations of mold catalase may be preserved against attack by bacteria byincorporating therein any suitable preservative, such as phenylmercurio nitrate or Merthiolate, f
Obviously, preservatives (such als-phenol) which inactivate catalase should not be used.
The solutions above described are extraordinarily stable throughout the pH range from 3.4. to 7.0. At pI-I 6.0, these solutionsretain not less than 90%` of their activity for at least 6A months, when kept at room temperature'in ordinary stoppered bottles. Ordinarily, Vthe losscf activity in 6 months is only a few per cent.
6.. Vacuum drying-The catalase in the concentrated aqueous solution obtained in step` 5 may be`r converted to 'dryjfor'm preferably by freezing thesolutionand subiimingt iii-vacuum, as fiori:
example.- tbeimethcd.- and apparatus described by Hays; and Koch, in Science, vol. 95 page 633 (June 19;., 1942);. Y
'Ihe'cflry preparation is .a pale green amorphous solidv of; low specific gravity, completely and easilyY solublein waterand aqueous solutions. .The solid preparation assays about 5,000 unitsvofcatalase activity per gram, andmay be stored atroom temperature for ,-ayear -or more .withl but slight loss of activity. ItV may be diluted with inertVA lieri such as dextrose., starch, or sodium chloride. tog, any convenient activity perV gram.
The Penicilliuni catalase obtainedby operating upin Penicillium` moldsl in accordance with the processv of Example I is a, new andvdistinct species of catalase having `its ,own unique and character` istic properties, such as molecular weight. isoelectricpoint, serum rcactions.` solubility. etc.. .distinguishing it from the previously known speciesV of; catalase. One of the important distinguishing characteristics of Penicillium catalase is its; exceptional stability upon aging,4 asabovede Another important identifying characteristic ofA Penicillinm catalase is its response to the pI-I of its environment. Penicillium catalase is irreversibly inactivated at pH 2.5, whereas beef liver catalase is inactivated at pH 3.0. Penicillium catalase is operative throughout the pH range from 3.0 to 10.5, and thev activity changes only gradually with changing pH. The relationship is quantitative and characteristic, so that Penicillium catalase may readily be identiecl by its activity-pI-l curve, which is shown in Figure 2 as curve A. This curve is drawn through the circled experimental values, determined at 0 C.
By way of contrast, curve B of Figure 2" shows the activity-pH relationship characteristic oi beef liver catalase, as. reported by Williams, J. Gen. Physiol. 11:309 (1928), upon tests conducted at 10' C.; under comparable conditions. As is apparent from Figure 2, Penicillium catalase retains more than.70%. of itsr maximum activity throughout the entire rangev of pH from 3.0 to 10.0, a span i of 10?. The activity of beef liver catalase, on the other hand, falls oi very rapidly as the pI-I is shifted from the optimum value 70% of its maximum activity persisting only in the comparatively narrow pH band from 5.7 to 8.1--a span of only 102A. Or, to state the matter in another way. Penicillium catalase is operatively efficient (to wit,
effective to more than 70% of its maximum activ-- The `process described in Example I producesV `a valuable yield ofvmold catalase when the raw material is Pem'ciZ/.m chryso-genum, Penicillum woatu'm, Aspergillus niger, spent Penicilliumfrom the production of penicillin, or spent Aspergillus obtained from the-production of either citricacid Thus Penicillium catalase isl Since the raw materials are biological products, they naturally vary from batch to batch. For that reason, some of the operating details may advantageously be adjusted in accordance with the results of laboratory-scale pilot operations performed upon each batch of raw material, in order to obtain maximum yield and purity. The nature and extent of these variations will be apparent from the following discussion of commercial operations upon Penicillium molds.
AutoZysis.-Penicillium molds autolyze readily when deprived of an adequate supply of oxygen and nutrients, even when not treated with a germicide. In commercial practice, however, it is desirable to use an antiseptic, not only to facilitate autolysis, but alsoto inhibit the growth of bacteria, such as the H2S generating micro-organisms, which inactivate catalase. A bacteriostatic concentration of the antiseptic is suicient. For the organic solvents, typified by toluene, an adequate quantity is 2% of the weight of the raw mold; for CuSO4-5H2O, 0.1% suices.
' I have successfully autolyzed mold throughout the temperature range from 10 C. to 40 C. The rate of autolysis varies somewhat with different batches of mold, but in general autolysis is completed within 24 to 48 hours at room temperature. Where it is desired to proceed as soon as the extraction of the catalase is complete, laboratory samples may be pressed from'the autolyzed slurry from time to time and assayed. Extraction is complete when the total catalase activity of the entire crude liquor, as calculated. from the assay upon'the laboratory sample, equals that of the original batch of mold.
Removal of acid-insoluble impurities may be effected at pH values between 3.5 and 4.5.
l Precipitation of cataZase.-Substantially all the catalase in the mother liquor is precipitated in the rst fractionation, if the ratio of acetone to mother liquor is between 2:3 and 1:1-l The quantity of co-precipitated non-catalase protein increases as this ratio increases, so that the crude catalase is contaminated with too much foreign protein if the ratio much exceeds 1:1. The catalase is precipitated by acetone throughout the pI-I range from 3.8 to 8.0, but maximum yield and maximum purity are obtained when the pH is between 4.5 and 6.0, and the ratio of acetone to mother liquor is between 2:3 and 1:1. The precipitation may be effected between C. and 40 C., but optimum results generally are obtained at room temperature. rIhis is a surprising and advantageous feature of the invention, since enzymes ordinarily are not recovered in good yield except at temperatures near 0 C.
Rza-precipitation of cataZcse.-Inorder to obtain a stable nal preparation, the second precipitation of catalase must be performed under fairly critical conditions. The temperatures may be the same as in the first precipitation. Where acetone is used at room temperature, the pH of the catalase solution should be between 4.0 andV 5.0. A pH of 4.5 uniformly gives good results, and may be employed routinely. The use ofv one-half volume of acetone then precipitates all the catalase without `co-precipitatingthe mpuri-.
fect the first precipitation of catalase, a protein fractionating solvent such as acetone should be employed to purify the catalase by re-precipitation, in order to obtain a Stable nal preparation,
Penicillz'u'm, notatum, pH '7, 1000 pounds, is diluted with water to a solids content of 15%; 1.5 pounds CuSO45H2O dissolved in a gallon of water is added; the resulting slurry is agitated for 2 hours, then allowed to stand at room temperature for 22 hours.
The autolysate thus formed is pressed in a hydraulic press at a pressure of pounds per square inch, thereby extracting the mother liquor. The pressed pad is re-extracted with water, and the washings are added to the mother liquor.
The mother liquor is adjusted to pH 7.0 with a weak base, such as NH4OH, to precipitate any acid-soluble matter, which is removed and dis-` carded. l Y
The pH of the 4partially claried mother liquor is adjusted to between 3.8 and 4.5 byslowly adding a dilute solution of a relatively weak acid, such as citric acid or acetic acid, and the liquor is allowed to stand for one hour. Acid-insoluble matter precipitates, and is removed, for example by centrifuging.
The claried mother liquor, amounting to 100 gallons, is adjusted to pH 6.0, and 500 pounds of ammonium'sulphate is added thereto, with stirring.
The crude catalase which precipitates contains 100% of the total catalase activity of the entire original batch of 1000 pounds of Penicil- Zz'um notatum. rlhis precipitate is separated by centrifuging or the like. Y
.The crude catalase is dissolved in 6 gallons of water, yielding a solution having a pH of about 5.5. The pH is adjusted to 4.3 with acetic acid, and'B gallons of acetone is mixed therewith. The purified catalase which precipitates is separated by centrifuging, and is dissolved in a mixture of 2 gallons of water and 2 gallons of glycerine to form a stable lconcentrated catalase preparation which requires no preservative and is suitable for use in food manufacture.
Example I II nAspergillus niger-'(strain No. 3, Northern Regional Research Laboratory) was grown sub\ merged with stirring and aeration in accordance with the conventional methods used in the production of penicillin. After 42 hours the mold- Was harvested by filtration and washed. The wet mold exhibited a pH of 5.9 and a catalase activity of 2.4 units per gram.
While young Aspergillus cultures, say 24 hours 1 old, autolyze readily, the older cultures frei The disodium phosphate buffer maintained the pI-I high enough to keep acid-soluble matter out of solution. At the end of this operation, the slurry was water thin.
The insoluble cell residues were removed by ltration and washed with water. The washings were added to the cell-free extract, giving a combined filtrate of 1400 ml., pH 6.6, catalase activity 1.0 unit per mil. Thus 74% of the total catalase activity of the mold appeared in thecrude mother 9 liquor. This liquor was cooled to 4 C. and added to an equal volume of acetone having a temperature of 20 C. The catalase which precipitated was collected on a filter, and 50 ml. of catalase solution was obtained by washing the iilter with water. The pH of this solution was 7.1 and its catalase activity was 59` units per nil. rlhus the total catalase activity oi the nal preparation was 140% of that of the crude mother liquor, and 104% of that of the mold from which it was prepared. The iinal preparation was extraordinarily stable, retaining 160% of its activity for 6 months, when stored at roo-m temperature.
The foregoing concrete examples, considered together `with the discussion herein, will enable those skilled in the art to obtain catalases from Penicillium, Aspergillus, and other molds. Having thus described and illustrated my invention, I claim:
1. The method of preparing catalase, which comprises: (1) treating Penicillium mycelium with an antiseptic selected from the group consisting of toluene, xylene, ethyl acetate, chloroform and copper sulfate, (2) autolyzing the dead mycelium, (3) adjusting the pH of the autoly- Zate to about 7, (4) ltering the neutral autolyzate to obtain a catalase extract substantially free of acid-soluble matter and undissolved cell residues, (5) changing the pH of said extract to between 3.5 and 4.5 to precipitate acid-insoluble impurities and removing the same, (6) adjusting the pH of the puried extract to between 4.5 and 6.0, (7) treating said purified extract with about an equal volume of acetone to precipitate crude catalase therefrom, (8) collecting said crude catalase and dissolving it in water, (9) adjusting the pH of the catalase solution to about 4.5, (10) treating said catalase solution with about one-half its volume of acetone to reprecipitate catalase therefrom, and (11) dissolving said catalase in water to obtain a stable solution thereof.
2. The process of claim 1 in which step (2) is accomplished between 10 C. and 40 C.
3. The process of claim 1, wherein steps (7) and (10) are each performed at temperatures between about 0 C. and about 40 C.
4. Process for the manufacture of catalase, comprising the steps of treating living Pencillium mycelium with toluene, thereby killing said Penicillium; maintaining the dead Penicillium at about room temperature, to autolyze the same; adjusting the pH of the autolyzate to about 7, thereby precipitating acid-soluble matter; filtering the autolyzed mass, thereby separating an extract substantially free of cells and acid-soluble matter; acidifying said extract, thereby precipitating acid-insoluble impurities; separating the acidifled extract from said impurities; treating said extract at about pH 3.8 to 8.0 with at least 2/3 volume of acetone, thereby precipitating crude catalase; collecting said crude catalase; adding water thereto, thereby dissolving said crude catalase; acidifying the solution thereby formed; treating the resulting acidied solution with about 0.5 volume of acetone, thereby reprecipitating catalase; collecting the re-precipitated catalase; and dissolving the same in a small quantity of water, thereby providing a concentrated stable solution of purified catalase.
5. A process for the separation of catalase from mold mycelium containing same, said mold being from a species selected from a genus consisting of Penicillium and Aspergillus, which comprises forming an aqueous suspension of said mycelium, autolyzing said mycelium in said suspension whereby the cell walls of said mycelium are disrupted to liberate the catalase therefrom and to form a solution containing catalase, separating solid mycelium residue from the resulting catalase-containing solution while maintaining the pH of said liquor to a value above about pH 6.0, thereafter adjusting the pH of said solution to a value between about pH 3.5 and about pH 4.5 whereby additional solids are precipitated, separating said additional solids from said solution, thereafter adding acetone to said solution While maintaining the pH thereof at a value between about 3.8 and about 8.0 whereby to precipitate said catalase, and separating the precipitated catalase from said solution.
6. A process for the separation of catalase from mold mycelium containing same which comprises forming an aqueous suspension of said mycelium, disrupting the cell walls of said mycelium whereby to liberate the catalase therefrom and to form a solution containing catalase, separatf ing solid mycelium residue from the resulting catalase-containing solution, thereafter adding a catalase-fractionating agent selected from the group consisting of acetone, methyl alcohol, ethyl alcohol and ammonium sulfate to said solution, the temperature of said solution being between about 0 and about 40 C. and the pH of said solution being between about 4.5 and about 6.0, whereby to precipitate said catalase from said solution, and then separating the precipitated catalase from said solution.
'7. The process of separating catalase from an aqueous extract of disrupted cells of mold mycelium which comprises acidifying said extract to a pH value between about 3.5 and about 4.5 to precipitate impurities, separating said precipitated impurities from the acidied extract, thereafter adding acetone to said extract while maintaining the pH of said extract at a value between about 3.8 and 8.0 at a temperature between about 0 and about 40 C. whereby to precipitate said catalase from the extract and separating precipitated catalase therefrom.
DWIGHT L. BAKER.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 525,832 Takamine Sept. 11, 1894 OTHER REFERENCES Loew, Dept. of Agri. Departmental Report, No. 68, Catalase, 1901, page 34.
Kastle, The Oxidases, Bulletin 59, Treas. Dept., G. P. O., Washington, 1910, pp. 135, 136, Bulletin 520.
Chem. Abstracts 21: 3915 (3) Compt. Rend. Soc. Biol. 97, 524-5 (1927).
Stern, Jour. Biol. Chem. 112 (1936), pp. 161- 169.
Chem. Abstracts: 35: 6732 (8) IX Hisao Matui, J. Agr. Chem. Soc. Japan, 16, 1064-70 (1940), Catalase of A. oryzae. X. Ibid. Catalase of molds and yeasts.
Advances in Enzymology, vol. I. (1941), Interscience Pub., Inc., N. Y., pages 172, 173.
Nord, Weindenhagen, Handbuch der Enzymologie II (1943), pp. 864-5.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US525832 *||Sep 14, 1893||Sep 11, 1894||The amies Pavement Company||Paving-block|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US2703779 *||Oct 23, 1953||Mar 8, 1955||Armour & Co||Method of preparing stable watersoluble catalase of high potency|
|US2926122 *||Feb 24, 1958||Feb 23, 1960||Dawe S Lab Inc||Method of preparing glucose oxidase|
|US3102081 *||Apr 18, 1960||Aug 27, 1963||Miles Lab||Enzyme precipitation process|
|US3114677 *||Jul 25, 1961||Dec 17, 1963||Stich Eugen||Fermentation apparatus|
|US3126324 *||Dec 23, 1957||Mar 24, 1964||Catalase compositions|
|US5362647 *||Feb 12, 1993||Nov 8, 1994||Allergan, Inc.||Compositions and methods for destroying hydrogen peroxide|
|US5521091 *||Jun 13, 1994||May 28, 1996||Allergan, Inc.||Compositions and method for destroying hydrogen peroxide on contact lens|
|US5766931 *||Dec 27, 1996||Jun 16, 1998||Allergan||Composition and methods for destroying hydrogen peroxide|
|US6022721 *||Feb 20, 1998||Feb 8, 2000||Development Center For Biotechnology||Catalase, the gene thereof and composition comprising the same, and process for preparing catalase using genetic engineering technology|
|US6022732 *||Apr 9, 1997||Feb 8, 2000||Allergan||Hydrogen peroxide destroying compositions and methods of using same|
|US7211249||Mar 17, 2003||May 1, 2007||Color Access, Inc.||Heat-generating composition for topical application to skin|
|US20040185023 *||Mar 17, 2003||Sep 23, 2004||Schnittger Steven F.||Modified heat-generating cosmetic compositions|
|DE1016669B *||Oct 18, 1955||Oct 3, 1957||American Cyanamid Co||Verfahren zur Herstellung eines proteolytischen Enzyms|
|EP0683677B1 *||Feb 9, 1994||Jun 18, 2003||Advanced Medical Optics, Inc.||Compositions and methods for destroying hydrogen peroxide|
|EP0870052B1 *||Dec 20, 1996||Feb 16, 2005||Genencor International, Inc.||Process for the preparation of gluconic acid and gluconic acid produced thereby|
|WO2004082603A2 *||Mar 10, 2004||Sep 30, 2004||Color Access Inc.||Modified heat-generating cosmetic compositions|
|WO2004082603A3 *||Mar 10, 2004||Aug 24, 2006||Color Access Inc||Modified heat-generating cosmetic compositions|
|U.S. Classification||435/192, 435/935, 435/816, 435/917, 435/936|
|Cooperative Classification||C12N9/0065, Y10S435/936, Y10S435/917, Y10S435/935, Y10S435/816|